Journal of Petrochemical Universities
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Particle Velocity Distribution in the Bubbling Fluidized Bed
YANG Kuan-li, WANG Qi-cheng, ZHANG Kai,DAI Wei-di,JIANG Jian-chun
Abstract439)      PDF (3355KB)(533)      
 
Radial velocity distributions of two kinds of glass beads, belonging to Geldart type B classification, were investigated at different axial sections in the bubbling fluidized bed with an inner diameter of 0.185 m under different superficial gas velocities. Local particle velocities were measured by using the PV-5A fiber-optical probe. The experimental results indicate that the radial distribution of particle velocities in the bed bottom zone is irregular, where the design of the distributor is dominated. When the axial section is far from the distributor, the particle velocities are higher in the center than those near the wall within the bed, which becomes obvious with increasing superficial gas velocity. Meanwhile, there exists a transitional zone between the above two zones, where the effect of the distributor tends to be weakened. This leads that the radial distribution of particle velocities is regular. Moreover, the amplitude of particle velocity at the same axial position changes sharply with an increase of superficial gas velocity.
2008, 21 (3): 5-8.
CFD Simulation on Homogeneous or Aggregative Fluidization of FCC Particles
LIU Wen-dong, ZHANG Kai, BI Ji-cheng
Abstract389)      PDF (1771KB)(607)      
Fluid catalytic cracking(FCC) plays an important role in the processes of the heavy oil refining industry. A thoroughly understanding of fluid characteristics in the gas-solid fluidized beds is helpful for designing the FCC units. A new two-fluid model developed by Brandani S and Zhang K is used to numerically investigate the hydrodynamics of FCC particles in the platform of CFX 4.4, a commercial CFD software package. Simulation is carried out in a two-dimensional fluidized bed with 0.25 m in width and 0.70 m in height. The particle with a diameter of 6.4×10- 5m and a density of 1 225 kg/m 3 is employed as solid phase. Two typical kinds of fluid dynamics, i.e., homogeneous fluidization and aggregative fluidization, are obtained under corresponding to superficial gas velocities, which are in good agreement with classical theories as well as experimental dates from the literatures.
2007, 20 (2): 43-46.